SIMULATION OF HYDROGEN SULFIDE DECOMPOSITION PROCESS IN MEMBRANE REACTOR

سال انتشار: 1382
نوع سند: مقاله کنفرانسی
زبان: انگلیسی
مشاهده: 1,824

فایل این مقاله در 9 صفحه با فرمت PDF قابل دریافت می باشد

استخراج به نرم افزارهای پژوهشی:

لینک ثابت به این مقاله:

شناسه ملی سند علمی:

NICEC08_014

تاریخ نمایه سازی: 8 اسفند 1386

چکیده مقاله:

A huge amount of H2S produces naturally in many gas wells and is often present in natural gas. H2S can be considered as resources for two salable, hydrogen and sulfur, production. The success in this field will result in waste minimization, resource utilization and environmental pollution reduction. Different technologies such as, thermal, thermo-chemical, electrochemical, photolytic and plasmolytic have been used in small scale for this purpose. In this study, firstly different processes for converting waste H2S to hydrogen and sulfur have been compared and the thermal-catalytic decomposition method followed by product removal by membrane is suggested to be one of the most practical and economical method for industrialization. Hysys package was used for simulation of a large scale H2S conversion membrane reactor to investigate effect of various parameters on hydrogen production yield. Results are shown that hydrogen yield has been decreased with temperature and molar flow rate increasing. The optimum temperature is between 600 to 650oC. Increasing of pressure difference between permeate and reaction side lead better hydrogen yield. As the major capital cost is related to membrane reactor, it is found that if the reactor structure is modified in which the specific area is maximized, the process will be more economic.

نویسندگان

Abdal

Faratech Co., Ghezelbash ۵, Tohid St, Isfahan-Iran

Karimi

Faratech Co., Ghezelbash ۵, Tohid St, Isfahan-Iran

Ehsani

Faratech Co., Ghezelbash ۵, Tohid St, Isfahan-Iran

Taherzadeh

Faratech Co., Ghezelbash ۵, Tohid St, Isfahan-Iran

مراجع و منابع این مقاله:

لیست زیر مراجع و منابع استفاده شده در این مقاله را نمایش می دهد. این مراجع به صورت کاملا ماشینی و بر اساس هوش مصنوعی استخراج شده اند و لذا ممکن است دارای اشکالاتی باشند که به مرور زمان دقت استخراج این محتوا افزایش می یابد. مراجعی که مقالات مربوط به آنها در سیویلیکا نمایه شده و پیدا شده اند، به خود مقاله لینک شده اند :
  • Zaman, J. and Chekama, A., "Production of hydrogen and sulfiur ...
  • Dowling, N.I and Clark, P.D., "Kinetic modeling of the reaction ...
  • H + _ «ه [3] Fan, J., et.al., "Effect of ...
  • Fan, J., "Analysis of a tWo-Stage membrane Reactor integrated with ...
  • Ohashi, H. et.al., "Hydrogen production from hydrogen Sulfide using membrane ...
  • Chan, P.P.Y., Vanidjee, K., Adesina, A.A., Rogers, P.L., "Modeling and ...
  • Gwaunza, M and Adesina A.A., "The performance of a Ru-Mo ...
  • Moffat, S.C., Adesina, A.A. , "The dissociation kinetics of H, ...
  • Faraji, F. et.al. _ "CO- catalyzed conversion of H, S ...
  • Faraji, F. et.al. _ "The CO- catalyzed conversion of H$S ...
  • Bolmer, P.W., 1966, U.S. Patemt 3409520 ...
  • Gauvin, W.H , "Novel reactor for plasma applications.", Chem. Eng. ...
  • Polak, L. , "Reaction under plasma condition", Wiley Interscience, New ...
  • C zernichowski, A. _ "Production of hydrogen from CHq, CO ...
  • C zernichowski, A., Lesueur, H., Czech, T. and chapel J., ...
  • Sanijuk, S.V et.al., "Complete valorization of H2S or H2S + ...
  • Argonne's Industrial Technology Development Division, Partner@anl.goy. ...
  • Buxbaum, R.E., Kinney, A.B., Hydrogen transport through tubular membranes of ...
  • Bolmer, P.W., 1966, U.S. Patemt 3249522. ...
  • Bolmer, P.W., 1966, U.S. Patemt 3409520 ...
  • نمایش کامل مراجع